Method of and apparatus for mixing and proportioning gases.



w. B. EDDISON. METHOD OF AND APPARATUS FOR NHXING AND PROPORTIONING GASES.

APPLICATION FILED NOV. H, 9X6.

Patented Feb. 18, 1919.

2 SHEETS-SHEEI' I.

W. B. EDDISON.

METHOD OF AND APPARATUS FOR MIXlNG AND PROPORTIONING GASES.

APPLICATION FILED NOV. 11. 19:6.

Patented Feb. 18, 1919.

2 SHEETS-SHEET 2.

' Inventor:

La Atty I UNITED STATES PATENT OFFICE.

WILLIAM BARTON EDDISON, OF IRVINGTGN, IiTEW' YORK, ASSIG-NOR TO THE SURFACE COMBUSTION CO., INCORPORATED, OF NEW! YORK, N. Y., A CGRPORATION QF NEW YORK.

METHOD OF AND APPARATUS FOR MIXING AND PRGPORTIONING GASES.

Specification of Letters Patent,

Iiatented Feb. 18, 1919.

Application filed November 11, 1916. Serial No. 130,887.

T 0 all whom may concern Be it known that I, l VILLIAM BARTON EoDIsoN, a citizen of the United States. re siding at Irvington, in the county of Westchester and State of New York, have invented certain new and useful Improvements in Methods of and Apparatus for Mixing and Proportioning Gases, fully described and represented in the following specification and the accompanyingdrawings, forming a part of the same.

This invention relates to a method and apparatus for mixing and proportioning gases, and more especially to a method and apparatus for supplying an explosive mixtureof air or other combustion supporting gas and a fuel gas in constant proportions to surface combustion furnaces at a ve locity suitable to the requirements of surface combustion.

The invention has been made With the Y object of providing a method and apparatus whereby a well mixed, homogeneous gaseous mixture may be conveniently supplied to the burner discharge orifices of a surface combustion furnace at a pressure above a pre determined minimum and in quantities variable at will and without changing the proportions of the constituent gases, that is, to meet the conditions of constant proportions, variable quantity, and exit pressure sufiicient to prevent backfiashing. A further object is to utilize efiiciently the pressure energy of one of the gases entering into the mixture for securing the supply of the mix-' ture at a pressure higher than that at which the other constituent gas is available.

The invention comprises a method wherein the pressure energy of a gas supplied under a relatively high pressure is changed in part to velocity energy with reduction of pressure, and'the other gas under a rela .tively low pressure is supplied to the stream of the inducing gas. at the place of relatively high velocity and low pressure, some of the velocity energy of the mixture thus produced then being changed back to pressure energy and the mixture being discharged under the desired pressure from the burner orifice; the flow of the inducing gas and the induced gas and the mixture all being controlled according to the flow law of orifices having constant coefficients, and the induced gas being supplied to the mixing In supplying an explosive gaseous mixturein accordance with my method and by my apparatus the air may and in many cases will be the gas which is supplied under pressure and which serves as the inducing gas, this for the reason that the air is usuaily the gas used in the largest volume and because in 'many establishments there is already installed and available a central supply or" pressure air and also because it is in some respects more convenient and desirable to handle air under pressure rather than the fuel gas. The fuel gas may, however, be used as the driving fluid, and may sometimes most desirably be so used, especially when supply of high pressure gas is available, or when, as with some weakgases, the gas volume is equal to or larger than the air volume used in combustion. For convenience in further description of the invention, it will be considered that the air is to be the driving or inducing gas.

The air, being then the inducing gas, is supplied under a sufiicient pressure past an adjustable restriction or controlling valve to a chamber from which it passes into a Venturi tube, that'is, a tubeer conduit of subing of limited angle between the, sides. In I passing through the entrance Leone .of the Vent-uri-tube, some of the pressure energy of the airis changed into velocity ener with reduction of pressure so that the lair passesthrou-gh the throat of "the Venturi tube with largely increased velocity and at a correspondingly reduced. pressure. The fuel gas, which may be taken at any avail-' able pressure from a suitable source, as from ordinary pipe at-fthe dietz ibuand low prc' under a suitable prt sure. which, while le.

tion line pressure, passes through a governing device which causes it to be supplied, at a pressure maintained approximately equal to that against which the mixture discl'iarged, tlr" t is, the furnace pressure, to be discharged no a nozzle orifice set to dis charge into the air in a region of relatively high velocity and low pressure in the entrance cone of the Venturi tube adj acent the throat thereof. is thereby induced, and the gas entering the stream of air at this point of high vclo *ity ure becomes thoroi Q'l'lly mixed with the H ll d as the mixtui then passes on through i e diverging portion, or pressure cone, of the Venturi tube velocity energy is conva v t id back into pressure energy so that the mixture passing on from the Venturi tube through a suitable relatively be supplital to the large conduit wid burner nozzle and barge orifice or orifices than that uialer which the air is sluii 'ilied, will be substantially greater than that under whi-zi'b the fuel iplit-d or the ordinary .lir' pre inc and :ater than the fur-- nace prtssurc. A homogeneous mixture of the :lucl and air will thus be supplied to the human. nozzle or orifice and will be disrhargcd under a suitable prev-sure tlurrefrom into a ful-nae! at a suitable velocit for preventin baclillashing through the banner orifice, so that, the mixture being an ex plosi one in re, surface con' lfuistimi thereof may taln lace as d sired. A re ..table for varying strictiou w -rich i the richn of the mixture desirably provided between the gas nozzle and the gas pressure governor.

'll ith the par s of the apparatus suitably formed and proportitmed, and. with the gas nozzle of suitable size in proportion to the Venturi throat according'to the .zharactcr of the fuel gas and suitably po ioned with relation to the throat, an explosive mixture of the fuel gas and air in the desired proportions may be obtained, and sucl'i proportions maintained ELPPI'OXlIIHLl/LLM constant under variations in the amour of mixture supplied resulting .troin variati the amount bf air smoplicd or the pressure under which the air reaches the entni 1W5 cone of the Venturi tube, so that "in practice the amount of mix ture of: uniform proportions supplied may be varied simply by adjusting the control valve or adjustable restriction past which the air flows to the supply chamber from the fan or other source'ol supply of air under suliicient pressure.

In order to maintain the proportions of fuel gas and air in the mixtureconstant under variations in air flow and amount oi.

A How of gas from the gas nozzle the tlow-controlling orifices; the Venturi tube has entrance and discharge cones of such limited angles that the gas will hug the sides ot the discharge cone and not jump away therefrom and set up eddy currents therein, and the pressure under which the fuel gas, that is, the induced gas, is supplied maintained substantially equal to the furnace pressure, or pressure against which the mixture is discharged from the burner orifices. The area of discharge nozzle or burner orifice or orifices should bear a suitable relation to the area of the Venturi throat; that is, the aggregate area of the discharge orifices should be small enough so that a proper or necessary pressure may be built up in the mixture flowing through the discharge or pressure cone of the Venturi tube, while yet icing large enough so that sufiicient pressure reduction may take place in the Venturi throat to induce the desired proportiv ate flow of the The development of back pressure resulting from the heating of the mixture in the burner orifice or orifices if the walls o'tthe orifices should become highly heated would, in the absence of some means for compeneating for the increase in back pressure, cause a change in the proportions of gas and air in the mixture. To avoid such upsetting of prmiiortions, the burner should be made'so that its orifice will have an approximately constant ircssurecapacity characteristic, and this may be secured by forming the burners or discharge nozzles so that the walls of the orifices shall be revented from becoming excessively heated In operation.

The explosive gaseous mixture supplied to a surface combustion furnace should be a homogeneous mixture. It is found that when gas is admitted to an air stream in ordinary pipes there-is little tendency to mix, especially if the quantities are large, and some means for mixing the gases has to be provided to produce a mixture suitable-foisurface con'lbustion. If, however, such unmixed streams of air and fuel gas in contact with each other are passed through a V euturi tube they emerge in a well mixed homogeneous stream as the result of the flow conditions which are peculiar to the double cone of the Venturi tube and without substantial loss of pressure. Itis also found that when the fuel gas is admitted above described to the throat ofalVcnturi tube through which a stream of air is passing, that a similar mixing action takes place and no additional mixing means is required, iv thoroughly well mixed homogeneous stream of the mixture being supplied even with the Venturi tubeclosely adjacent to the burner discharge orifice. I

By the term surface combustion as used ibhe n ure 1 l of illlldilimfii eemhusi'iei is disclosed lhurles E. Luclie among i .l-vi'liii'cli 22, lllOaiy 1915. iiiveniieu. ed (lQSC .ip'cien of an nbedyiug up r 111". iii; the method and of the and such 9. deseripsion cenueejen he ees showing such an "not an apparatus made the iuventien with the eel? shown in section; 21011 partly breken away er such shown in Fig.

n Opellllig i011 insin- '"euist one "ell sectional View i. tube and the gas hail sectional View skewing of means i? couti'elliug e mixture; and

tionel View showing lame I first to serve as )lied uni"; Fun ewe!" 19, us

; lug air bei iig supplied. l supply pipe or conduit 11. te 21 ch 1.1"? be." and an adjustable gestrieiaion 01' g p'revided in the supply pipe F m the supply if air to the and he pressure maintained. Ironi ene Te of the 7 er 12 is a Venturi tube rune bf which opens into lillfi n the end of the discharge delivery pipe 16 leads 0 e or mil ljilifi diseliuyge ori means fol ceuirellii'ig the uieens, the fuel ue will trance 50 the Veniuuri tube t0 insure an even flew the air from all sides iute the enmance eene of the Veuiuri tube.

The fuel Teen any suitable source of supply is led elu'oug i a. supply pipe 20 to u piessure governer which reduces its pressure to mi of atmosphere or other pressure appi-oxiuiete equal to the internal furnace pressure, an fiem the goveruer the gas under the cleaned pressure passes through a pipe te he (liSClltl'lQQd from an outlet orinerzzle 23 nto the throat of the e. The gevemor may be of any r ion. The form which l s suewn in the drawings, is

* '0"51'1101' having a. con- 1 \lllCll iFOI'THSDHQ side 7 W ieithe iszidi'uitted :11 Whi h is eonnected with the diuphnigui eln'eugh its pivoted supporting lever to he ceuirelled thereby in the usual Way The other side (if the diaphragm '"rubjec 'l ire u liuid pressure which determines em :11? in he maintained Within as by having an inelosing as shown formed, as I mm a. free epening; 28 so uic we sure will be 11minthe chamber 29 provided by euvh e: sing. if, hewevei: the furnace pressure is or less than eri'mosphere, then the de zl'iullingg pressure against the gGVGIDUP die mgm may be obtained in a simple manner by n'ieuns 0i :1 tube 30 slieu'n in Fig. 1 leading from the furnace chamber to the opening 28. The casing inclosine; the diaphragm on its outer side being then a tight cz sing ihe diupluugm will be :11: all times subjecied i0 :1 pressure equal to the furnace m me whether tlii seine be constuui- Gl' varying. flush connecting tube may of course be eu'ipleyed when the furnace pressure is thui :i'f uhunsphei'e, but is not fihen necessary. By such preesure governing always be supplied to the connecting supply pipe 22 under a pressure n'niintninMl equal 1'10 the iucernal furnace pressul'e, that is, the pressure against which the explosive mixture is discharged fromfiehe burner nozzles mdischai-ge orifices;

r The l eniuri iuhv must he of suitable form and of suitable limited angles between the sides ofiiis erti'unuo and discharge cones erg? of ihe driving gas may he efficiently enmloyed to supply the mixture under the Astant within the working range of flow rates,

desired. pressu The stream of r passing through the throat has a h gh velocity. and the stream will not hm; or ii smoothly along the Sides of the discharge cone 35 if: the included angle between. the sides is too great. Too great an angle between the sides will therefore result in the frn'inat'ion of side or eddy currents. This is objectionable since conversion of velocity back into pressure in the discharge cone requires regular red action of the velocity without side or eddy currents in order to be ellicicntly done, that is, in order to develop the maximum rise in pressure c0nsistent with or corresponding t the decrease in velocity. l urthermore, the presence of such eddy currents rcsnlis in a variation in the position longitudinally of the tube of the point of minimum jet cross-section under variation in the rate of flow. Such change in. location of the point of minimum jot cross-section would interfere with the maintenance of constant proportions of the constituent gear in the mixture since it would mean a corrcspomling change in location of the point of maximum velocity and minimum pressure, which is at the point of mini mum. jet cross-section and would, therefore, not remain in mual'ant or fixed position at the minimum cross-section or throat of the tube. (in the other hand, too small an angle would mean an. excessive length of the coneand involve exec-sire friction losses. An angle. of 10 between the sides has been found to work well under usual conditions of operation with t] a air supplied under a. pressure of two or three pounds.

If the included anglev of the entrance cone 36 is too large, the air stream leaving the entrance cone will not lill the throat and first part of the discharge con-e, out will jumpclcar of the walls making a so-called contracted rein (rr/mcomma-ta.) and set up eddy currents, which, in addition to pre venting full recovery of pressure equivalent to the loss in velocity, interfere with the proportionality element by causing under variations in quantity of air flowing a move ment longitudinal "of the tube of the point of maximum velocity and minimum prcssure, the location of which determined by the minimum cross-scction rather than by the minimum cross-section or throat of the tube. Such movement of the point of maximum velocity and minimum pressure under variable rates ol': flow must be avoided and the location of this point must be maintained constant for all rates of flow within the normal range of: the apparatus in order that constant prol'iortions may be maintained. To secure this result, the angle between the sides 0 the entrance cone and the 'llori'nation or the cone must be such that its coeliicient of discharge will be con and desirably n'actically 100%. lt has been found in practice that an angle of approximately 46 between the sides works well, and such an angle is considered best with the air supplied at a pressure of 2 or 3 pounds and with the apparatus otherwise constructed as shown. might be used, but if the angle is too small the air supply will encounter excessive friction in reaching the throat, although it would otherwise arrive all right. A comparatively short entrance cone is sufficient and the entrance diameter is not important, provided, however, that the cone should be long enough to give the required direction to the entering stream of air. A length equal to one'half the diameter of the throat has been found to work well. The sides of the entrance cone should, of course, curve gradually to the throat.

The Venturi tube should, therefore, have its entrance and discharge cones of such limited angles that the air or other gas will hug the sides of the discharge cone and uniintain the position of the point. of minimum jet cross-section stationary at the throat of the tube, and that the desired rise in pressure will be developed, and the necessary change of velocity energy back into 1 are ener'j will be effected without excessive friction losses. The flow through the tube will be controlled by the entrance cone and throat according to the flow law of orifices, change in the pressure maintained in the supply chamber 12 causing change in flow with pressure drop and velocity increase at the throat according to such orifice flow law, without interference by varying coefficients of flow or velocity of entrance or discharge.

The gas nozzle 23 being set to discharge into the throat of the Venturi, a flow of gas therefrom results by reason of the depressed pressure which exists in the Venturi throat, and also probably somewhat through the e'ntraining efl'ect of the air flowing past the cndof the nozzle. The nozzle orifice should have an area of suitable size for passing the proportionate amount of fuel gas desired with reference to the amount of air flowing, and, most desirably, should, when the inducin Vcnturi throat am the induced gas to the nozzle, be set back from the oint of mini mum throat cross-section o the Venturi tube a distance, depending on its outlet area, so that the area between the nozzle outlet and the walls of the Venturi entrance cone is substantially the same as the area of the A smaller angle gas is supplied to the eas es Same as would be the conditions of flow or form as to have a co-eflicient of working into the throat at its minimum diameter from a gas nozzle occupying no space; allowance being made, however, for the volume of the space occupied by the entering fuel gas in the center of the air stream,

which can be corrected for by enlarging the throat by an amount equivalent to the area of the entering stream of fuel gas, orby moving the, gas nozzle back from the minimum throat diameter not quite'so far as corresponds to zero gas flow.

The gas nozzle is made of such form, and the connecting supply pipe 22 between the nozzle and the pressure governor is of such relatively large size, that the flow through the nozzle will be in accordance with the flow law of orifices, and this nozzle or flow controlling orifice shouldbe of such shape discharge which'is {approximately constant within the ow range, as in the case of the entrance cone of the Venturi tube, in order that, adjustment being once made for the desired proportionate amount of fuel gas to the air for a given flow rate, the proportions will not vary for other flow 'rates by reason of variance .in coeiiicients, that is, the nozzle should have a suitably rounded and tapered entrance and the orifice beyond the tapered entrance should be straight, or slightly tapered and as short as will cooperate suitably with v other parts of the structure. The nozzle should also have a sharp discharge edge so as not to interfere with the air fiowand to avoid eddy cur rents at the outlet.

The position of the fuel gas nozzle with respect to the Venturi throat may be varied so1neWhat,-and such variation in position will have the eficct of; and may be de pended upon for, changingthe proportions of the constituent gases in the mixture, or the richness of the mixture, movement of the nozzle inward or toward the throat increasing the richness of the mixture, and movement outward giving a leaner mixture. To provide for such relative adjus ment between the nozzle and Venturi tube,

the nozzle may be adjustahly mounted as shown in'Fig. 1. But movement of the nozzle inward from the best or most ellicient position means loss of efiiciency of the apparatus, and I consider it most desirable, therefore, under some conditions to have the nozzle remain in a fixed position and to provide other means for adjusting for change in proportions. An adjustable mounting of the nozzle such as shown may be employed for settingthe nozzle the position in which it is to remain, out ally it is not necessary to provide any such adenine means for this uurreee.

I; L ,t"..

the nozzle longitudinally inward or outward course be accomplished by such change of nozzles.

It is desirable, however, that means be provided for adjusting proportions within limits without necessitating change of nozzles, and so that such adjustment may be made conveniently and while the apparatus is in operation. For this purpose, means for adjusting the nozzle 23 operable from outside the casing of the chamber 12 may be provided, and Fig. 4 shows such a means consisting of a' rod 37 extending through the wall of the gas passage and a suitable stuffing box and carrying a hand wheel, whereby the threaded collar which carries-the nozzle may be turned to cause it to move to adjust with respect to the-Venturithroat. Other means may also bexprovided for this purpose. For example, a nozzle may be used having an adjustable outlet area. Such a nozzle 23 is shown in Fig; 5, in which the outlet area of the nozzle is varied by adjusting the position of a flow-controlling wedge 40. Such a nozzleshould of-course 'be formed, as it may be in about the form shown, to

have a coefiicient of discharge which is constant, or approximately so, within the work ing range of flow. Away in which; now consider it best, however, under certain conditions, to provide 'foradjustment of proportions while the apparatus Is in operation,

and which I wish to claim in this application, is to provide an adjustable restriction formed to serve as a flow-controlling orifice of constant coefiicient form placed the connecting pipebetween the gas nozzle and thegovernor. Such an adjustable fiow con trolling orifice or restriction is provided in the apparatus as shown in Figs. 1 and 4 by the valve 45 having its valve head and seat so formed as to provide an orifice having an approximately constant coefliclent of d1scharge. When this valve is partly closed so that in the operation of the device. a drop in pressure will occur past the valve, the amount of gas passing through thenozzle 2 3 will of course be less than when the valve is wide on under which conditionno such drop in pressure takes place; By. adjust? merit of the valve, therefore; proportions oi th constituent gases in thefmixturo deliv-- cred from the Venturi tube may be varied as desired, and this is accomplished without interfering with the maintenance of proportionality under different rates of mixture supply since all the flow controlling orifices have the same flow law and the same or constantcoefficients. It sometimes desirable to provide both the adjustable restriction in the gas supply passage and the nozzle ad usting means.

The furnace, partly shown in Fig. 1, and a broken section of which is shown in Fig. 2, an impact-jet, surface combustion furnace for burning explosive gaseous mixtures in accordance with the method of U. S. Patent No. 1,146,724, granted July 13, 1915, on an application of Charles F. Lueke. lhe furnace comprises a structure providing a furnace chamber 51 in which is located one or more porous and permeable comlnistion supporting beds 52 of suitablerefractory material against which jets of the explosive gaseous mixture are directed from nozzles 53 which are set in the furnace wall and which are supplied with the explosive mixture through connections from the delivcry pipe 16 leading from the Venturi tube of the mixing apparatus. The jets of the explosive gaseous mixture, moving with a velocity in excess of the rate of propagation of inflammation of the mixture, strike against the combustion supporting beds by which the mixture is deflected and caused to spread out with rapid loss of flow veloclty, and combustion of the mixture takes place at the surface of or Within the bed as described in said patent.

The burner nozzles 53, like the gas and air controlling orifices, have discharge orifices of constant coeflicient :l'orm. and the connecting passages between such orifices and the Venturi tube, including the delivery pipe 16, its branches, and the nozzles pas-- sages leading to their discharge orifices, are all of such relatively large that there will be no or substantially no pipe resistance to affect the flow of the mixture. The con-- necting pipe 22 between the gas nozzle and the gas chamber 25 of the governor be ing also of. such relatively large size as to avoid pipe resistance. the flow of the air and of: the "fuel gas and of the mixture will, there'l'm'c, all be controlled only by orifices torn-led described, and whatever pressure drop occurs in the apparatus must be through an oritire with vclo. ily and n'cssurc cl'zange according to the typical flow law of orilicos, and not by reason of pipe, bend or eddy cu rrcn t losses.

If, however, the burner nozzles should in the operation. of the furnace become so highly heated as to increase the. back pressure by reason of heating of the mixture as it llows through. the nozzles, this would, in

the absence of means for com mnsating therefor, have the. effect of changing the proportions of the mixture. Such increase in back pressure by increasing the pressure in the expansion cone of the Venturi, tube would result in a, reductirm in the flow velocity through the Ventu'ri throat and a reduction in the proportiomnte amount of fuel gas enterin; the threat from the nozzle 23. Such heating of the mixture in the burner nozzles is also had in that it reduces the amount of mixture flowing from the nozzle under the available pressure. It dcsirable, therefore. to employ nozzles formed. to prevent such heating of the mixture, that is, to use nozzles having an approximately constunt pressurecapacity characteristic under varying furnace temperatures, 2'. (a, nozzles the capacity of or volume of flow through which under any given pressure is the same for different furnace temperatures to which the nozzle is exposed, or which have a constant flow coellicient regardless of furnace temperatures, and to avoid the use of noz zles having varying! pressure-capacity char-- actoristics, unless other means are provided for overcoming the ell'ect of such nozzles on the maintenance of proportionality.

The desired constant pressurwcapacij v characteristic of the nozzles may be secured by forming the nozzles so that the tempera ture of the walls of their mixture passages will be prevented from becoming excessively high. For this purpose the nozzle should be so formed and mounted as to limit the amount of heat of combustion which will be taken up by the nozzle and to cause such heat as is taken up by the nozzle to be rapidly conveyed away so as to prevent any portion of the wells of the mixture passage of the nozzle from becomirm unduly lumted.

This result is acctmiplished in the nozzles of the furnace shown in the drawings by havmg the nozzles formed and. set in the furnace wall so that only a small portion of: the end or nose of the nozzle is exposed to the furnace heat, the balance thereof being protcctcd by the surrounding wall of material which is a poor hea t conductor, and by forming the nozzle of a body of metal of suflicient continuous mass to rapidly conduct away to the outer portions of the nozzle body such heat as is absl'u'hed by the exposed nose of the nozzle, and by forming the outer end of the nozzle body with means for discharging the heat, such as the heat dissipating fins or plates 54, for taking; away and discharging the heat to the atumsphere. It desirable that a limited annular portiol'i of the metal about the discharge orifice of the nozzle be exposed to the interior of the furnaee in order that no part otthc relatively noircomlucting material forming thev flll nace lining shall be in immediate contact with the gas stream issuing from the nozzlel' since this material because of its D001 heat lilo conduetingquziities becomes in operation of the furnace heated to inosiideseesee, if extended over the end of the nozzle so to be in contact with the stream of mi would cause ignition of some of the mixtuii, at this "point with resulting creeping heck of ignition more or vless Within the nozzie passage and consequent heating: of the mixture Within the passage. with o nozzle formed anti set as deseribeci and'as shown in Fig. 2 oi the drawings, excessive "rise in temperature of the WltiiS of the iiozzie passage such as would substantially aiiiect the maintenance of proportionality iii the mixture may be effectually avoided. The prevention of the Waiis of the mixture (liseharge nozzle becoming unduly heated. is also of importance-in avoiding back flashing of on explosive mixture which would occur it the walls 01" the larger portion of th Where the mixture moves more sioi 'iy should become heated to the ignition tem 'iemture.

In U. S. Letters Patent No. 1 "1,1142, dated October 2 1917, Richerdsom \JSOH and Read, there is disclosed and oiaimeii means such as described abeve for discharg ing the stream of mixture to be burned In this application no claim is made to such means per se, but only. as pert of apps-- ratus forsuppiying a mixture of approximately constant proportions.

The total area. of the discharge orifices of the burner nozzles supplied with ml tore from the mixing apparatus should a suitable relation to the capacity the pa-ratus, and especially to the cross of the Venturi throat. Too great an aggregate area of the burner iiisohzirge'olifioes Wouid prevent the buiidin g up of LhG'jlQCQSSiIlY mixture pressure for causing the requireti excess Veioeity of dis-:harge item the 11oz zie's, and too small an aggregate ill is of the discharge orifices Wouit prevent sufficient pressure reduction at the Venturi thio I have found it ciesii'zibie in WOZil'iiiQ; with on air pressure of two or three pounds that the aggregate area of the burner discharge orifices should not be more than about twice the cross area of the Ventui'i throat. it should also be noted that. any change in the aggregate area of the burner discharge ori- .fic'es, such as a change in the number of burner nozzles supplied, Wiii of course have a corresponding effect on the proportionaiity offthe-mixtfire. i

In the operation of the appemtus, the air b'eingsupplied under suitehle'pressum :mri the apparatus being mijust'ed to secure the desired proportions for any" flow rate, then the amount of mixture suptoiieii may be varied as ciesiz'eci within the v limits of the apparatus be simply H ei vei've 13, the pwpoi'tions of a. i maintained substantially With opening and, closing of the val ve.

' sure than the ot-heii to ear P -:1 new and fuif ileci. I well mixect, homog pointed out.

Whiie ini'eiitir "i he? as embodied in an e induced is supp QDTH-liiii stream imi the mien; the (iii/i119; ga s beizi nozzie and e intiih, ing :iiinuiai posse it may sometimes be C es the-(ii'ivi :i ziiiabi consta cost-ice oiific'e is to be u;

coefficient of diseiie mately constan. range of the'eppei'o ess 0 of the contrecte-ii vein U stent. has been so efi'ieients the ices of the pi'oximsteiy range oft-ho for reasons eoei fioient of proxiinateiy is I What is chimed is: I r 1. The method pYCiizCiiEg m6 s ing a mixture of in oppi'o constant proportio whi plying one of ti Q ses u gas, changing some of pressure we sue-h inducing as to web energy rednetioii oi ii'e. sup hing; the as three 5.71 of the iniiu w outlet orifice to the high velociiiig at a DOiIli 0i y eiict Row some of the ieioeiiy ens he to pressure ens the disc-in: a

2. The method of producing and supply ing a mixture of gases in approxin'lately constant proportions, which con'lprises supplying one of the gases under a higher pressure than the other to serve as an inducing gas, changing some of the pressure ener'gy of such inducing to velocity energy with reduction of pressure, supplying the other gas, under a pressure approximately equal to the pressure against which the mixture is discharged, to the stream of the inducing gas at a point of relatively high velocity and low pressure, changing some of the velocity energy of the mixture back to pressure en.- ergy, controlling the flow of the induced. gas and the mixture according to the flow law of orifices having constant. coefficients, and varying the quantity of mixture supplied by varying the supply of the inducing gas.

The method of producing-and supplying a mixture of gases in approximately constant proportions, which comprises supplying one of the gases under a higher pressure than the other to serve as an inducing gas, changing some of the pressure energy of such inducing gas to velocity energy with reduction of pressure, supplying the other gas through an outlet orifice to the stream of the inducing gas at apoi'nt of relatively high velocity and low pressure, changing some of the velocity energy of the mixture back to pressure energy, discharging the mixture through. a discharge orifice, maintaining the supply pressure of the induced. gas approximately equal to the pressure against which the mixture is discharged .from the discharge orifice, varying the. quantity of mixture supplied by varying the sup-- ply of the inducing gas, and varying the proportions of the inducing and induced gases in the mixture by adjusting a flow controlling orifice in the passage through which the induced gas flows to said outlet orilice.'

4. The inethodpf supplying an explosive mixture of fuel gas and combustionsupportinggas in approximately constant proportions to a surface combustion furnace, which comprises supplying one of the gases under a higher pressurethan the other to serve as an inducing gas, changing some of the pres-- sure energy of the inducing to velocity energy with red uctionof pressure, sup plyin g the other gas, under a supply pressure approximately equal to the internal furnace pressure, to the stream of the inducing gas at a point of. relatively high velocity and low pressure, changing some of the velocity energy of the mixture back to pressure energy, and controlling the flow of the induced gas and the inducing" gas and the mixture according to the flow law of orifices having constant coel'lieients;

5. The method of supplying an explosive, mixture of fuel gas and combustion smiporh ing gas in approxhmttely constant. pr0portions to a surface comlimstion furnace, which compris supplying one of the to the entrancecone ot' a Venturi tube formed to maintain the point of minimum jet crosssection stationary under varying flow rates, supplying the other gas through a constant coefficient orifice discluu'ginq into the en trance core of the Venturi tube in the direc tion of flow through the tube, one of said gases being supplied under pressure to serve as an inducing gas and the other being supplied under a pressure approximately equal to the internal. furnace pressure, and control ling the flow of the mixture from the Venturi tube into the furnaceaccording to the flow law of orifices having constant coefiieients.

6. The method of supplying an explosive mixture of. fuel gas and combustion supporting gas in approximately constant proportions to a surface comlmstion furnace, which comprises supplying one of the gases to the entrance cone of a Venturi tube :t'ormed to maintain the point of minimum -jet section stationary under varying flow rates, sup lying the other gas through a constant coe cient orifice discharging into the on trance cone of the Venturi tube in the dime tion of flow through the tube, one of said gases being supplied under pressure to serve as any inducing gas and the other bein supplied under a yn'essure approximalcly equal to the internal furnace pressure, and controlling the floW 'ofthe :nir-rture from the Venturi tube into the furnace according to the flow law of orifices having constant co-- ctlicients by means of a dracha-rge passage having an approximately constant pressurecapacity characteristic'un ler varying turnace temperatturcs.

7. The method of prmlucing and supplying a mixture of gases in appr iximately com stunt prrmortimls, which comprises supplying one of the gases to the ntrance cone of a Venturi tube having its entrance cone, throat and dis hzurgc cone .t'ormed to avoid eddy currents in the gases llou'uig there constant coellicient. orifice discharging into the entrance cone of the Venl-uri tube in. the

direction of flow through the tube, the gas supplied to the entrance cone of the Vcuturi, tube being supplied under prcssurc to term as an inducing gas and the other {Ia eiug supplied midcr a pressure approxiumtely equal to the pressure against which the mixture is discharged, discharging the mixture from and controlling its flow by a constant UlGfllClGnh orifice, and varying the nuuu'zity of mixture discharged. by \"a ryin the amount of the inducing gas supplied.

8. The method of supplying an explosive mixture of fuel and combustion. support-- ing gas in approximately cruuaaut proper tions to a surface comlnistien turn: i which formed t0,controllingits comprises forming the mixture by supplying one of the-gases under a higher pressure than the thane serve as an inducing gas, changing some ofthe pressure energy of the inducing gastove'locityenergy with reduccharging it -in-to the furnace through, a con- ;stant coeflioient orifice having 'an approxifurnace, Which comprises flchanging some of the pressure energy of the inducing gas to locity and low. pressure,

mately constant pressure-capacity character-v istic under varying furnace temperatures.

9. The method of supplying a mixture of fuel gas and combustion supporting gas in approximately constant proportions to a forming a mixture with the aid of inducing action of one of the gases supplied under a relatively high pressure onthe other-gas supplied under a relatively low pressure, and supplying the mixture as formed to, controlling its flow by, and discharging itinto the furnace through, a discharge passage having an approximately constant'pressure capacity character istic under-varying furnace temperatures.

10,. The method of supplying an explosive mixture of fuel gas and combustion supporting gas in approximately constant proportions to a surface combustion furnace, Which comprises supplying the combustion, supporting gas under a higher pressure than the: fuel gas to serve as an inducing gas,

velocity energy with reduction of pressure, supplying the fuel gas through a constant coefficient orifice to the stream of the combustion supporting inducing gas at a pointoi': relatively high vechangingsome of the velocityenergy of the mixture back to pressure energy, controlling the flow of the the flow law of orifices the supply pressure of the fuel gas approximately equal tot-heinternal furnace pressure.

11. The method of supplying an explosive gaseous mixture of fuel gas and combustion supporting gas in approximately constant proportions to a surface combustion furnace raving an internal pressure other than atmospheric, which comprisessupplying one of the gases under ahigher-pressure than the other to serve as an inducing gas, changing some of the pressure energy of the in ducing gas to velocity energy with reduction of pressure, supplying the other-gas a supply pressure approximately equal: to furnace pressure to the stream of theinducing gas at apoint of relatively high velocity and low pressure, changing flow by, and dis-.

, velocity energy or sure energy, and means for-controllmg-the ilovv of the mixture according-tofthe flow,

some of velocity energy of the mixture back to pressure energy, and controlling the How of the mixture according to the flow law of orifices having constant coefiicients.

12-. Apparatus tor producing and supplying a mixture of gases in approximately constant proportions, comprising in combination means for supplying one of the gases under a higher pressure than the other to serve as an inducing gas, flow controlling means adapted to change some of the pressure energy of such inducing gas to velocity energy With reduction of pressure, means providing an outlet orifice set to-di'schar'ge into the stream of inducing gas at a pointofrelatively high velocityand low ressure' and in the direction of flow thereo for supplying the other gas to said outlet orifice under a pressurev approximately equal 4 which the mixture is for changing some of to the pressure against discharged, and means the velocity energy of the mixture back to pressure energy. 13. Apparatusior producing and supply-- ing a mixture of gases in approximately comprising in comblconstant proportions, nation means for supplying one ofthe gases under a higher pressure than the other to serve as aninducing gas, flow controlling means adapted to change some of the pressure energy of such inducing gas to velocity energy with reduction of pressure, means means providing an outlet orifice set to discharge M into the stream of inducing gas at a point of relatively high velocity and low ressure and in the for supplying the other gas to said outlet orifice under a pressure approximately equal to the pressureagainst whichthe mixtureis discharged, means for changing some of the the mixture backto pres energy with reduction of pressure, means providing an outlet orifice set to discharge into the stream of inducing gas at a point of,

relatively high velocity and low pressure for supplying-the other gas to said outlet orifice under a pressure approximately equal to'the pressure against which the mixture, is discharged, means for changing some oil the, velocity energy or" the mixture back to pressure energy, means for controlling thefiovv ot'the mixture according to the flow lavv of orifices having constantcoeilicients,

direction of flow thereo means the i and in the direction of flow thereof, means and. foruvarying the iPPl of the Q inducizg gas to vary the quantity 0 mixture 'suppli' v I 5. Apparatus I I ing'a mixture of gases in approximate 3 constant pro ort 1ons,comprising in combination. a enturi tube formed to main- 1 4 1 the point of jet'cross-section I stationary under varyli inhg into the entrance cone of the Venturi tu flow rates,' means roviding-an outlet 0 ce set to dischar "'in'the'direction .of flow through the tube a. connections for supplying. 7 "to the; entrance cone of the enturi tube. and Ptosaid orifice respectively, means for supplying one of sai I w s'e'rve as the driving "as, means providing faconstant coefiicient ow-controlling orifice i ,for controllin the flow-of the gaseous mix- 20* otlier of saidjgases 'under a pressure apses to bemix gases' under pressure to tureflprod-uce means for. supplying the! proximately equal "to i the pressure againstl lvvh'i'ch the mixture is dischargedzfrom said? ing ythesu'pply; of-the drivinfigas vary] roviding un outlet ori ce set to dischar' s m w s, rs pp s to'the' entrance noneo I and to said orifice respectively i -fsupplying one of said gases un "trolling the pressure un er' whichitlie other is suppliedand means prov dingajfl'ow ycon'trolling oriii .theTaseousmixture'produced. -;1 Apparatus forp'roducing and-siippl intolthe'entjrance cone of-thezVenturi tu --in the direction" f. flow through-the mt "t e m x t vie s meansfor.

'der ressure to's'ei've as .thedriv ing' means ce for controlling the flovvof constant proportions, comprising in combinato maintain. thetiojnja Venturi-tube f citubeqmeansfor'su pl sawa ned Venturi tubeunder P1766 'm a s 3 point of minimum etcross-seeu n hgi y in comm-m j cie tinutl fi es t wh under'varyin flow rates, means p charge into'theent'ranoe coneof the Venturi tubei -the' direction-of now through the vi -;a. constant a "orificethrou h-jw'hichtlie'mixtureireceivedirom otthe' V ifthe i so the,

enturi tube is discharged, andmeans {for g maintaining the initial pressure of last mentionedgas'app'roximately. equal to p v forproducing and suppl w cone and discharge flow rates, meansl and the connections.

Aga n v. -.tl ie-mixture discharged from saidlast' mentioned-prificet plying a mixture of in approximately constant proportions, comprising in coma nozzle set to discharge into the entrance cone of the Venturi tube in the direction of bination a Venturi tube having its entrance cone of limited angles,

flow through the tube, means for sup lying I one of vthe gases under pressure to e en- I trance cone of the Venturi tube to serve as the inducing gas, means' forsupplying another gas to said nozzle under a pressure approximately 31131 to that a 'nst which t e mixture'is controllingthe flow of the mixture; the en-' trance cone of the Venturi tube and said nozzle and said meansfor controlling the harged, an means forflow of the mixturebeing all formed a control the flow of the gas to the flow law of orifices having constant coefii:

cients, and the connections between saidparts of the apparatus being formed and Eerogortioned to-substantially avoid" p P i n I I and eddy losses. I ni An-apparatus' for producing and an I plying a mixture of gases in approximate y jconstant proportions, compris ng in coin:

cone and discharge coneof limited angles, a nozzle. set to dischar into the entrance cone of the Venturi tu e in'the direction of oneof the gases under pressure to the en- 'the inducing gas, means for supplying. another gas to said nozzle'under ajpressure v approximately equal-to'that instwhi'ch the mixture is discha 5 an controlling the flow of e mixture; the en- "{tranfce cone of the Venturi. tube and said' nozzle and said-means. for controlling the 'fl'ou of the'mixture being all formed to conmeans for 1 fbination a Venturi tube having its entrance I .v 9 flow through the tube, meansxfor supplying trance cone of the Venturi tube to serve as trol the flow of thegas according to the flow llawiof, orifices ha constant cmfli'eie'ntsf formed and proporthe'a paratus ,tion tosubstantia ya'void pipe bend and eddydo'ssesjfandladjusting means for vary ing the supplyof 'the 'inducingafas to vary the quantityoi mixture suppli 20 Apparatus for producing and burning aniixturejof fuel gas and combustion sup (porting gas in approximately constantgxo' I portions, comprising in combination a Charge cone of; imited angles,.a

. .i z e "set to discharge into the entrance throughthe tube, means'for' under pressure ,to e entrance cone 0 Yentur'i tube to serve as the. in;

I equal to that a ninst whichthe mixture-is "discharged, "and a burner nozild throu li I'i tube havin its entrance cone and diseen saidpartslo '1 ndbfihev Venturi-Wbe in the direction of How.

ark-i sid '8 'f'ducin gas,meansfor supplying the other gii's' to'sai nozzle under a; pressure approximately" #RQWee -iP essM isb i the. m x an d hm I orifices having constant coeiiicients, connections between said portinggas in apprpxiinatelj cm 80 teristieunder yarying'temperaturesto ch ;,it'1s exposed.

ture offuel B5 gaS i-n approximately min the operation-oi which one ofthe gases" than the l 40 flows as-it is prodnced having a (llis it is produced burned; the entrance cone of the Venturi tube and said gas nozzle and said burner.

nozzle being allforrned 'to-control the flow turi tube in the direction of to .hc flow law cat and the ,he mlxe'djt'o the entrance coneoi the through them according parts the apparatus 'being formed and proportioned to substantially avoid pipe, bend and eddy losses,

and the burner nozzle having an approxi-' 10 matel constant pressure-capacity character istic under yarying temperatures to which it is ex o sedg I ff 21.1, pparatus for producing and bin a mixture of. incl ga'sfand comb H portions, comprising a; Vent -Ji'l to to maintain the point or' minirnum j 'et c section stationary under varyingfic'yw '1 H means providing an outlet-orificeset to dis? inthe direction of flow through for supplying ithe ases theVen-i turi tube and to said orifice respectively;- and the; tube, connections to be mixed to the entrance cone of flow-controlling discharge'ori'fice of con stant coefficient and 'i'wfhich h an approximately, constant pressure-capacity [charac- 22.j'The combination with" apparatus for producing and supplying an explosive mix; gas and combustion supporting constant" proportions a Tgreat'er pressure other'exerts a ,flOiY inducing action on the other gas, eta burner P h chthe mixturesupplied under orific'eoif constant coefficient and of tippr'oxi inately constant pressure capacity characfteIlSt-lC.

2;}. The cornhination ivithapparatu for intmtheentrance producing and supplying an erploswei'ni'ii' ture of fuel gas andcombustionsupporting- 20 charge), into the entrance cone of the "Yentigiriaryundmc turi tube 25 aburner tube to which the mixture flow's'as' controlling. means for i gas in approximately constant proportions,

of a-iburner to which the mfiiiture flowsas it is" produced having a discharge-orifice oiconstant coefficient/ and approximatelyponstant reassure-capacity characteristic. p 24-. he combination W1 h apparatus i01 producing and supplying an explosive mixture of, fuel gas and combustionsupporting ply, v I

gas in approximately. constant proportions equal to the pressure against which the mixfiows asture is stant proportions, comprising .in combination a Venturi tube formed to maintain the constant proportions,

point of minimum jet cross-section stationiiiga c'onstantcoetlicient orifice set to discharge into the entrance cone of the Veutube, connections for supplying sureunde'rjwhich'thedriving gas is supplied towary the amount of mixture produced without changing the proportions of the constituent gases therein.-

- 2 Apparatus'forproducing and supply a "mixture of gases in approximatelv constant'proportions', comprising in comht nation a: Venturi tube termed to maintain. thdpoint of minim-11in ,jet cross section stavarying; :flow rates. nozzle having acoustant ccefiicient orifice set to discharge into the entrance cone of the Von. t'uri tube in the direction oi'i flow throu' h the {511133, connections for supplying the u s to a: flow-controlling constant for controllincthe new of produced, adjustable varying the press .i'e under-whichthe driving gas is supplied to vary the-amount of mixture produced withoutchanging the proportions of the constituent: gases thereim and means adj ustahle for means providing. coefiicient orifice the gaseous mixtur varying-the proportionate amount of ,gas

flowing from said nozzle.

2'72 Apparatus for producing and sup inga mixture of gases in up roxiinately I 'stant proportions, comprisingin coinhinin arge V nturi tube formed to maintain the point of: minimumjet cross-section stationary under rarying flow rates, a nozzle having a constant co'efiicient orifice set to discharge cone of the fi enturi tube in the direction of flow through the tube means providing-a flow-ccn trolling orifice for controlling the flow of the gaseous miriture producedmmeans b undera higher pressure to serve-as thje driving gas; plying the other gas controlling-means formaintaining the suppressure of such other gas appro u atcly than the other c means for supdischarged, and an adjustable restr-iction between said pressure controiling means and said nozzle for varying the pro portionate amount of gas flowing from the nozzle.

28. Apparatus for producing and supplying a mixture of gases in approximately comprising in combination a Venturi tube formed to maintain the point of minimum jet cross-section stan L? m xed to the entrance cone of the v on s it-js produced, said burner tubeqhaf nngf a turntube and to said nozzle respectively} to said nozzle, pressn1 e;

for supplying one of the ases to the entrance cone of the Vent-mi tn oecharge into the entrance cone of the Venturi tube in the direction of flow through the. ,tube, means provi s flow-controlling Q constantfcoefiicient ori ceLfor controlling the d between said nozzle an the; Venturi tube-for:

meintaimngthe supply pressure of other gas'approximatel equal to. the pres- 0 mm s.

.as thef'drrrmg the 1 means or maintaining suppyresale,- of the gas supplied to said om iih m m 'mqtely equal to the pressure which Jan for underwhich the drivinggsa'is-supe than chnngi th 2 1 Py 1 the ozmstituent gases first, means edvsure char and means forvarying' the ropes? 0 min flow of the gaseous mixture produced, means for supplying one of the u trance cone of the Ventun tube 'under 'e higher pressure thantheother serve ,Apmssu' is "con the mixture. is discha I causing a relative Ion tudinal ldiustment fjvaryin the proportionate at; flowin from the nozzle. pp s us s -ing a mixture of gases in approximetelyoom jstant roporting-hconzpusmg tion eent'uri point of etipros's-se'etim ary under varying owrates, nouhhsving a constant coeflicient to discharge into the entrance tuhef in the directionfof flow" through orifice for total the flow; of-the ous mixture p u means orsupp one of the asesto theentranoe wn under ,a higher pressure nozzle, pressure controllm'g means. I for v such 'contro'llmg the flow of the 'mi xturefromthej Venturi tube intothefurnace-sccording'to- 90 by the inteb. h pressure forf naintaining the supply presmre ofjthe. gas supplied to said ately equal; to the internal- .1 not" .-In'-teaimony whereof I have hereunto set V hand in the presence of two subscribing' Vehturi tu the other gas tose'rv'e as the driving "means for supplying the'other gas to inst which tionate amount of gas flowing zle com rising means for causing-5.18M;

ulongitu inal adjustment between the nozzle 3 ,and the Venturi tube and an .adjkltlble stri'ction between the nozzle and said- 1');

sure controlling means.

ing emlxture of gases in *appronmg the point of minimum jet cross-section sta' sett'o dischar tothe en-' 1 ,mstely equsl cone of the Ventut'hlfitube, meansjpmvifling i 30. Apparatus for producing I. Witnesses:

tionary uh'derrarying'flow-ra't'esfa nozzle into the entrance cone of the Venturi tubein ,the dire'ction of flow through the tube, connections for supple the turi said. nozzle respectively, means-for supplying one of said gases .under pressure tes'erveas the dri'vi controlling means for maintaining. the sup- My f off the other gasapproxito the pressure which a means providing llingorificeior controlling the. produced; ail-t usteble'cont'ro means forveryingthe ilied'tov thef t emmsce, a Venturi, tube. formed to maint P i 1 m m ie memos s e'tions yuniler varyug new: rattan, a gauge I clen- 0 0e: 1,

'55 l to be'mixed'to thee'ntrenoe cone 0 the" ,en-"

10 i i .thef-pro"rtionete mmsmfi on some the tum in"; e as o? 'in appro xi?n ately constant P'OPOHSIM'CDIIIPl'lBIHQ in-"conibinstio with sure to serve as the driving gas,-meansfor the flow. lew of orifices havi constant 00-. zeficie'n i Pd' means oontr'ollz a s?? furnace pressure.

JomwIH.Benmm,-ilr., 

